Vis enkel innførsel

dc.contributor.authorGao, Hongxia
dc.contributor.authorLuo, Xiao
dc.contributor.authorCui, Ding
dc.contributor.authorLiang, Zhiwu
dc.contributor.authorHu, Xiayi
dc.contributor.authorHartono, Ardi
dc.contributor.authorSvendsen, Hallvard Fjøsne
dc.date.accessioned2019-02-26T12:15:39Z
dc.date.available2019-02-26T12:15:39Z
dc.date.created2018-12-11T14:04:22Z
dc.date.issued2018
dc.identifier.citationAIChE Journal. 2018, 64 (6), 2078-2088.nb_NO
dc.identifier.issn0001-1541
dc.identifier.urihttp://hdl.handle.net/11250/2587458
dc.description.abstractThe liquid film thickness and hydrodynamic entrance length in a vertical tube was studied experimentally and numerically. Measurements using distilled water, 30 wt % MEA and 40 wt % sugar solutions were carried out to investigate the effects of liquid flow rate on the formation of the liquid film. The experimental results validate the new Navier-Stokes based equation in cylindrical coordinates (Eq. 16) and the volume of fluid (VOF) model giving a competitively high prediction of the liquid film thickness especially in the low Reynolds number region. In addition, a new empiricalmodel and an improved minimal surface model have been first proposed for calculation of the hydrodynamic entrance length, with a relatively reasonable average absolute relative deviation (AARD) of 3.03% and 6.83%, respectively. Furthermore, the effects of the hydrodynamic entry length on the gas–liquid interfacial area calculated by the improved minimal surface model were comprehensively studied, and can be ignored if the ratio of the liquid film length (y) and the hydrodynamic entrance length (kE) is lower than 10. However, it should be noted that the hydrodynamic entrance length cannot be ignored in packed columns in which the liquid flow is very complex due to the packings with different structures and materials.nb_NO
dc.language.isoengnb_NO
dc.publisherWileynb_NO
dc.titleA study of film thickness and hydrodynamic entrance length in liquid laminar film flow along a vertical tubenb_NO
dc.typeJournal articlenb_NO
dc.description.versionsubmittedVersionnb_NO
dc.source.pagenumber2078-2088nb_NO
dc.source.volume64nb_NO
dc.source.journalAIChE Journalnb_NO
dc.source.issue6nb_NO
dc.identifier.doi10.1002/aic.16081
dc.identifier.cristin1641719
dc.description.localcodeThis is the pre-peer reviewed version of an article, which has been published in final form at https://doi.org/10.1002/aic.16081. This article may be used for non-commercial purposes in accordance with Wiley Terms and Conditions for Self-Archiving.nb_NO
cristin.unitcode194,66,30,0
cristin.unitnameInstitutt for kjemisk prosessteknologi
cristin.ispublishedtrue
cristin.fulltextpreprint
cristin.qualitycode2


Tilhørende fil(er)

Thumbnail

Denne innførselen finnes i følgende samling(er)

Vis enkel innførsel